JPH08143704A - Vinyl chloride resin composition - Google Patents

Vinyl chloride resin composition

Info

Publication number
JPH08143704A
JPH08143704A JP6290767A JP29076794A JPH08143704A JP H08143704 A JPH08143704 A JP H08143704A JP 6290767 A JP6290767 A JP 6290767A JP 29076794 A JP29076794 A JP 29076794A JP H08143704 A JPH08143704 A JP H08143704A
Authority
JP
Japan
Prior art keywords
vinyl chloride
acid
zinc
chloride resin
pentaerythritol
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP6290767A
Other languages
Japanese (ja)
Other versions
JP3440584B2 (en
Inventor
Takeo Tanaka
丈夫 田中
Yasuyoshi Miyaji
保好 宮地
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ajinomoto Co Inc
Original Assignee
Ajinomoto Co Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ajinomoto Co Inc filed Critical Ajinomoto Co Inc
Priority to JP29076794A priority Critical patent/JP3440584B2/en
Publication of JPH08143704A publication Critical patent/JPH08143704A/en
Application granted granted Critical
Publication of JP3440584B2 publication Critical patent/JP3440584B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Abstract

PURPOSE: To obtain a nontoxic vinyl chloride resin composition having good heat stability by mixing a vinyl chloride resin with a zinc stabilizer and a polyhydric alcohol stabilization aid having a low content of unreacted pentaerythrotol. CONSTITUTION: This method for preparting the polyhydric alcohol stabilization aid consists of mixing a dibasic acid (e.g. adipic acid) with 3-7mol, per mol of its anhydride (e.g. phthalic anydride), pentaerythritol, subjecting the resultant mixture to a dehydrative condensation reaction at 150-230 deg.C to remove (n-2) to (n) mol equivalent or below water when a dibasic acid is used or remove (n-2) to (n) mol equivalent or below water when the anhydride of a dibasic acid is used. The method of preparing the vinyl chloride resin composition consists of mixing 100 pts.wt. vinyl chloride resin with 0.1-10 pts.wt. zinc stabilizer such as a Ca-zinc and/or a Ba/zinc stabilizer (e.g. a metal soap in which the fatty acid moiety is a stearic acid, and the metal moiety contains Ca and Zinc) and 0.1-10 pts.wt. polyhydric alcohol stabilization aid.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は熱安定性良好な塩化ビニ
ル系樹脂組成物、さらに詳しくは塩化ビニル用多価アル
コール系安定化助剤に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vinyl chloride resin composition having good thermal stability, and more particularly to a polyhydric alcohol stabilizer for vinyl chloride.

【0002】[0002]

【従来の技術】塩化ビニル系樹脂は低廉かつ優れた物性
を有することから、水道管、建材、電線被覆材、日用
品、家具、玩具、医療用輸液チェーブを始めあらゆる分
野で使用されている。従来の塩化ビニル系樹脂は、熱ま
たは太陽光を始めとする光線等で劣化分解し易いので、
これを防ぐため、鉛系、カドミニウム系、錫系等の安定
剤が配合されていた。ところが、最近は環境保護の立場
から毒性のある鉛系、カドミウム系等の重金属系安定剤
は敬遠され、規制されるに至っている。
BACKGROUND OF THE INVENTION Since vinyl chloride resins are inexpensive and have excellent physical properties, they are used in all fields including water pipes, building materials, electric wire coating materials, daily necessities, furniture, toys and medical infusion chaves. Since conventional vinyl chloride resins are easily degraded and decomposed by heat or light rays such as sunlight,
In order to prevent this, stabilizers such as lead-based, cadmium-based, and tin-based stabilizers have been added. However, recently, from the standpoint of environmental protection, lead-based, cadmium-based, and other heavy metal stabilizers, which are toxic, have been shunned and regulated.

【0003】これらを解決する手段として、無毒または
低毒なカルシウム−亜鉛系、バリウム−亜鉛系、マグネ
シウム−亜鉛系等の亜鉛系や錫系の安定剤へ移行しつつ
ある。しかしながら、亜鉛系安定剤を配合した塩化ビニ
ル系樹脂組成物は、一旦劣化分解が始まると塩化亜鉛が
生成し、この塩化亜鉛が塩化ビニル系樹脂の劣化を更に
促進するいわゆる亜鉛焼け現象を引き起こすので、これ
を防ぐため多価アルコール系安定化助剤を併用配合する
ことが良く知られている。多価アルコール系安定化助剤
としては、ペンタエリスリトール、ジペンタエリスリト
ール、トリペンタエリスリトール等の多価アルコールが
効果的と言われるが、実際にはこれらの多価アルコール
は融点が高く、塩化ビニル系樹脂との相溶性が悪いため
熱安定性効果が不足したり透明性低下を招くため、カル
ボン酸で部分エステル化して使用する方法が数多く提案
されている。
As a means for solving these problems, non-toxic or low-toxic zinc-based stabilizers such as calcium-zinc based, barium-zinc based, and magnesium-zinc based stabilizers are being used. However, a vinyl chloride resin composition containing a zinc stabilizer produces zinc chloride once deterioration and decomposition start, and this zinc chloride causes a so-called zinc burning phenomenon that further accelerates deterioration of the vinyl chloride resin. In order to prevent this, it is well known that a polyhydric alcohol-based stabilizing aid is used in combination. As the polyhydric alcohol-based stabilizing aid, polyhydric alcohols such as pentaerythritol, dipentaerythritol, and tripentaerythritol are said to be effective, but in reality, these polyhydric alcohols have high melting points and Since the compatibility with the resin is poor, the thermal stability effect becomes insufficient and the transparency is deteriorated. Therefore, many methods of partially esterifying with a carboxylic acid to be used have been proposed.

【0004】たとえば、特開昭55−69639、特公
昭57−61289や特公昭61−47866には、ペ
ンタエリスリトールや、ペンタエリスリトールを脱水縮
合したポリペンタエリスリトールを種々カルボン酸で部
分エステル化して成る塩素含有樹脂用安定剤が開示され
ている。しかし、上記におけるペンタエリスリトールと
カルボン酸の反応におけるモル比は、概ね1:1〜3:
1であり、その結果得られた反応物の分子中の水酸基含
量では、実用的な安定性効果の点で十分ではないことが
知られていた。そこで本願発明者が上記実施例を追試す
ると、ペンタエリスリトール脱水縮合物には、未反応の
ペンタエリスリトールが30〜40%含有すること、さ
らに脱水縮合をすればする程褐色に着色するという傾向
があることが判明した。さらに該脱水縮合物2モルに対
しアジピン酸を1モル用いてエステル化した反応物には
低分子量で昇華性も高い未反応のペンタエリスリトール
が20〜30%も残存していることが判った。
For example, JP-A-55-69639, JP-B-57-61289 and JP-B-61-47866 disclose pentaerythritol and polypentaerythritol obtained by dehydration condensation of pentaerythritol by partial esterification with various carboxylic acids. Stabilizers for containing resins are disclosed. However, the molar ratio in the reaction of pentaerythritol and carboxylic acid in the above is about 1: 1 to 3:
It has been known that the content of the hydroxyl group in the molecule of the resulting reaction product is not sufficient in terms of practical stability effect. Therefore, when the inventors of the present application re-test the above-mentioned examples, the pentaerythritol dehydration condensate contains unreacted pentaerythritol in an amount of 30 to 40%, and tends to be colored brown as the dehydration condensation is further performed. It has been found. Further, it was found that 20 to 30% of unreacted pentaerythritol having a low molecular weight and high sublimability remained in the reaction product obtained by esterification with 1 mol of adipic acid based on 2 mol of the dehydrated condensate.

【0005】実際、多量の未反応のペンタエリスリトー
ルが存在する脱水縮合物を、硬質塩化ビニル系樹脂に配
合すると、加工時に於いて昇華にともなう作業性の問
題、加工機の汚染、又、配合組成物の透明性や耐衝撃性
低下といった問題が生じていた。 こうした点で、従来
知られているペンタエリスリトールや、その誘導体と種
々のカルボン酸との反応物は、安定剤として充分な性能
を有しているとは言い難かった。又、ジペンタエリスリ
トールとアジピン酸の部分エステル化物に関しては、耐
衝撃性や熱安定性効果には優れるものの、融点が高く分
散性に問題があり、結果としてその透明性に関して問題
を有していた。即ち、塩化ビニル系樹脂組成物に於いて
亜鉛系安定剤を配合する場合、安定化助剤として従来用
いられていた微粉砕ジペンタエリスリトールや、ジペン
タエリスリトールとアジピン酸の部分エステル化物を主
成分とした種々の多価アルコール系安定化助剤を加える
と、その熱安定性効果、配合物の透明性、配合時の作業
性等の観点のうち何らかの問題が生じ、これらの問題点
全てを満足する多価アルコール系安定化助剤が切望され
ていた。
In fact, when a dehydration condensate containing a large amount of unreacted pentaerythritol is blended with a hard vinyl chloride resin, there is a problem in workability due to sublimation during processing, contamination of a processing machine, and a blending composition. There have been problems such as transparency of products and deterioration of impact resistance. In this respect, it has been difficult to say that conventionally known reaction products of pentaerythritol and its derivatives with various carboxylic acids have sufficient performance as a stabilizer. Further, the partial esterified product of dipentaerythritol and adipic acid has excellent impact resistance and thermal stability, but has a high melting point and a problem of dispersibility, resulting in a problem of transparency thereof. . That is, when a zinc-based stabilizer is blended in a vinyl chloride-based resin composition, finely ground dipentaerythritol conventionally used as a stabilizing aid or a partial esterification product of dipentaerythritol and adipic acid is used as a main component. Addition of various polyhydric alcohol-based stabilizing aids causes some problems in terms of their thermal stability effect, transparency of the compound, workability during compounding, etc., and satisfies all of these problems. There has been a long-felt need for a polyhydric alcohol-based stabilizing aid that can be used.

【0006】[0006]

【発明が解決しようとする課題】本発明の課題は、塩化
ビニル系樹脂に亜鉛系安定剤と併用配合する未反応ペン
タエリスリトールの含有量が少ない多価アルコール系安
定化助剤を提供し、物性良好な塩化ビニル系樹脂組成物
を得ることである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a polyhydric alcohol-based stabilizing aid having a low content of unreacted pentaerythritol, which is used in combination with a vinyl chloride resin in combination with a zinc-based stabilizer, and has physical properties. It is to obtain a good vinyl chloride resin composition.

【0007】[0007]

【課題を解決するための手段】ペンタエリスリトール
や、その誘導体とカルボン酸とを反応させる時の適正な
モル比、その脱水反応条件、脱水反応の終点管理法、反
応物中の組成等について詳しく検討を行ったところ、
1.ペンタエリスリトールが10wt%より多く含有し
た、多価アルコール系安定化助剤を塩化ビニル系樹脂に
配合した場合、配合量にもよるが、該塩化ビニル系樹脂
組成物の加工時にペンタエリスリトールが昇華し、加工
機の汚染や、それに伴い該塩化ビニル系樹脂組成物製品
の肌荒れ現象等が懸念され、従って、該多価アルコール
系安定化剤中のペンタエリスリトールの含有率は10w
t%以下であることが必須であること、さらに、2.多
価アルコール系安定化助剤の合成に於て、アジピン酸ま
たはフタル酸等の2塩基酸に対し、ペンタエリスリトー
ルを大過剰用いて反応させ、反応時の脱水量を調整する
ことにより該多価アルコール系安定化剤中のペンタエリ
スリトールの含有率が10wt%以下である優れた安定
化助剤が得られること、並びに、3.それを用いて塩化
ビニル系樹脂組成物製造すると、作業性も向上すると共
に得られた組成物の性能も優れていることを見い出し
た。
[Means for Solving the Problems] Pentaerythritol or its derivative and a proper molar ratio when reacting with a carboxylic acid, dehydration reaction conditions, control method of dehydration end point, composition in reaction product, etc. are examined in detail. I went to
1. When a polyhydric alcohol-based stabilizing aid containing pentaerythritol in an amount of more than 10 wt% is blended with a vinyl chloride resin, pentaerythritol is sublimated during processing of the vinyl chloride resin composition, depending on the blending amount. It is feared that the processing machine may be contaminated and the vinyl chloride-based resin composition product may be roughened, so that the content of pentaerythritol in the polyhydric alcohol-based stabilizer is 10 w.
t% or less is essential, and 2. In the synthesis of polyhydric alcohol-based stabilizing aids, pentaerythritol is reacted with a dibasic acid such as adipic acid or phthalic acid in a large excess to adjust the dehydration amount during the reaction. 2. An excellent stabilizing aid having a pentaerythritol content of 10 wt% or less in the alcohol-based stabilizer can be obtained, and It has been found that when a vinyl chloride resin composition is produced using it, workability is improved and the performance of the obtained composition is excellent.

【0008】即ち、本発明は2塩基酸またはその無水物
1モルに対し、3モル以上7モル以下のペンタエリスリ
トールを触媒の存在下、脱水縮合を行い、2塩基酸の場
合はn−1モル当量以上n+1モル当量以下の水を脱水
させ、2塩基酸の無水物の場合はn−2モル当量以上n
モル当量以下の水を脱水させて得られることを特徴とす
る多価アルコール系化合物である。上記の反応で得られ
る多価アルコール系化合物はペンタエリスリトールの含
量が10重量%以下である。さらに本発明は、塩化ビニ
ル系樹脂100重量部に対し、カルシウム−亜鉛系やバ
リウム−亜鉛系安定剤等の亜鉛系安定剤を0.1〜10
重量部、該多価アルコール系反応物を0.1〜10重量
部を配合することを特徴とする塩化ビニル樹脂組成物で
ある。
That is, in the present invention, 3 mol or more and 7 mol or less of pentaerythritol is dehydrated and condensed in the presence of a catalyst with respect to 1 mol of a dibasic acid or an anhydride thereof, and n-1 mol in the case of a dibasic acid. In the case of an anhydride of a dibasic acid, n-2 molar equivalents or more and n
It is a polyhydric alcohol compound obtained by dehydrating water in a molar equivalent or less. The polyhydric alcohol compound obtained by the above reaction has a pentaerythritol content of 10% by weight or less. Further, in the present invention, a zinc-based stabilizer such as a calcium-zinc-based or barium-zinc-based stabilizer is used in an amount of 0.1 to 10 relative to 100 parts by weight of the vinyl chloride resin.
A vinyl chloride resin composition, characterized in that 0.1 to 10 parts by weight of the polyhydric alcohol-based reaction product is blended.

【0009】本発明に用いる塩化ビニル系樹脂組成物の
合成に於て用いる2塩基酸は、アジピン酸、コハク酸、
マレイン酸、マロン酸、フタル酸、イソフタル酸、及び
テレフタル酸等のごく一般的な2塩基酸で良い。モノカ
ルボン酸では、多価アルコールとの反応で、より高い水
酸基含有率を得るのに困難であり、3塩基酸以上のカル
ボン酸では、多価アルコールとの反応で容易にゲル化す
るので反応終点の管理が困難である。又、本発明に於い
ては、原料として先に述べた2塩基酸の無水物すなわち
無水フタル酸、無水コハク酸、無水マレイン酸、無水マ
ロン酸等を用いる事もできる。本発明の原料である2塩
基酸類、ペンタエリスリトールの形態は、溶融状態で反
応させるため、粉末状、フレーク状等のいかなる形態で
あっても問わない。
The dibasic acid used in the synthesis of the vinyl chloride resin composition used in the present invention includes adipic acid, succinic acid,
Very common dibasic acids such as maleic acid, malonic acid, phthalic acid, isophthalic acid, and terephthalic acid may be used. With monocarboxylic acids, it is difficult to obtain a higher hydroxyl group content by reaction with polyhydric alcohols, and with carboxylic acids with 3 or more basic acids, reaction with polyhydric alcohols easily gels, so the reaction end point Is difficult to manage. In addition, in the present invention, the above-mentioned dibasic acid anhydride, that is, phthalic anhydride, succinic anhydride, maleic anhydride, malonic anhydride, or the like can be used as a raw material. The dibasic acids and pentaerythritol, which are the raw materials of the present invention, may be in any form such as powder and flakes because they react in a molten state.

【0010】また、本発明に用いる酸触媒としてはりん
酸、硫酸、パラトルエンスルホン酸、スルファミン酸等
が挙げられ、これらを単独または併せて用いても構わな
い。酸触媒の添加量は、0.05wt%以下では、反応
速度が遅く、5wt%以上では、反応速度がそれ以上速
くならず、0.05〜5wt%で十分である。
Examples of the acid catalyst used in the present invention include phosphoric acid, sulfuric acid, p-toluenesulfonic acid, sulfamic acid and the like, and these may be used alone or in combination. If the addition amount of the acid catalyst is 0.05 wt% or less, the reaction rate is slow, and if it is 5 wt% or more, the reaction rate does not further increase, and 0.05 to 5 wt% is sufficient.

【0011】本発明の多価アルコール系安定化助剤の合
成するには、ペンタエリスリトールと2塩基酸に対し、
酸触媒を添加し、150〜230℃で所定の脱水量を得
れば良い。反応温度は、150℃未満では反応速度が遅
く、230℃より高い温度ではペンタエリスリトール自
身の脱水縮合混合物が生成し易く着色の原因となり、望
ましくは、180〜225℃である。所定の脱水量は、
ペンタエリスリトールと2塩基酸のモル比がn:1(n
は 3≦n≦7)の時、n−1モル当量以上、n+1モ
ル当量以下である。脱水量がn+1モル当量より多い場
合では反応が進行しすぎるため反応液がゲル化してしま
う。また、脱水量がn−1モル当量未満では未反応ペン
タエリスリトール含有率が10Wt%より多くなってし
まう。従って最適の脱水量はn−1モル当量以上、n+
1モル当量以下である。たとえばペンタエリスリトール
6モルと1モルのアジピン酸との反応では所定の脱水量
は5モル以上7モル以下である。
In order to synthesize the polyhydric alcohol-based stabilizing aid of the present invention, pentaerythritol and dibasic acid are added to
It suffices to add an acid catalyst and obtain a predetermined dehydration amount at 150 to 230 ° C. When the reaction temperature is lower than 150 ° C., the reaction rate is slow, and when the temperature is higher than 230 ° C., a dehydration condensation mixture of pentaerythritol itself is liable to be generated, which causes coloring, and is preferably 180 to 225 ° C. The predetermined dehydration amount is
The molar ratio of pentaerythritol and dibasic acid is n: 1 (n:
When 3 ≦ n ≦ 7), n−1 molar equivalent or more and n + 1 molar equivalent or less. If the dehydration amount is more than n + 1 molar equivalents, the reaction proceeds too much, and the reaction solution gels. If the dehydration amount is less than n-1 molar equivalent, the unreacted pentaerythritol content will be higher than 10 Wt%. Therefore, the optimum dehydration amount is n-1 molar equivalent or more, n +
It is 1 molar equivalent or less. For example, in the reaction between 6 mol of pentaerythritol and 1 mol of adipic acid, the predetermined dehydration amount is 5 mol or more and 7 mol or less.

【0012】又、本発明に於いて原料として先に述べた
2塩基酸の無水物を用いた場合、合成条件は2塩基酸を
用いる場合と全く同様であり、ペンタエリスリトールと
2塩基酸の無水物に酸触媒を添加し、150〜230℃
で所定の脱水量を得れば良い。所定の脱水量は、ペンタ
エリスリトールと2塩基酸の無水物とのモル比がn:1
(nは 3≦n≦7)の時、n−2モル当量以上、nモ
ル当量以下である。脱水量がnモル当量より多い場合で
は反応が進行しすぎるため反応液がゲル化してしまう。
また、脱水量がn−2モル当量未満では未反応ペンタエ
リスリトール含有率が10Wt%より多くなってしま
う。従って最適の脱水量はn−2モル当量以上、nモル
当量以下である。たとえば、ペンタエリスリトール6モ
ルと1モルの無水フタル酸との反応では所定の脱水量は
4モル以上6モル以下である。又、本発明に於いては、
原料として2塩基酸及びその無水物を複数種類混合して
用いることは全く問題なく、2塩基酸と無水物の混合で
あっても良い。その場合の、反応終点を決定する脱水量
は、混合物のモル比より計算で容易に求めることができ
る。
When the above-mentioned dibasic acid anhydride is used as the raw material in the present invention, the synthesis conditions are exactly the same as those when the dibasic acid is used, and pentaerythritol and the dibasic acid anhydride are used. Acid catalyst is added to the product, 150-230 ℃
It suffices to obtain a predetermined amount of dehydration. The predetermined dehydration amount is such that the molar ratio of pentaerythritol and the anhydride of dibasic acid is n: 1.
When (n is 3 ≦ n ≦ 7), it is not less than n−2 molar equivalent and not more than n molar equivalent. If the amount of dehydration is greater than n molar equivalents, the reaction proceeds too much and the reaction solution gels.
If the dehydration amount is less than n-2 molar equivalents, the unreacted pentaerythritol content will be higher than 10 Wt%. Therefore, the optimum dehydration amount is n-2 molar equivalents or more and n molar equivalents or less. For example, in the reaction between 6 mol of pentaerythritol and 1 mol of phthalic anhydride, the predetermined dehydration amount is 4 mol or more and 6 mol or less. Further, in the present invention,
There is no problem in mixing a plurality of dibasic acids and their anhydrides as raw materials, and a mixture of dibasic acids and anhydrides may be used. In that case, the dehydration amount that determines the reaction end point can be easily obtained by calculation from the molar ratio of the mixture.

【0013】又、本発明に於いて、分子中の水酸基含有
率を高めるため、2塩基酸に対するペンタエリスリトー
ルとのモル比をできるだけ上げることが望ましいが、モ
ル比が7より大きい場合は、反応時に所定の脱水量を得
るために、長時間脱水反応を行う必要があり、その結果
反応の進行と共に着色が目立つようになり、所定の脱水
量を得た段階では実用面で耐えられない着色度となる。
又、モル比が3より小さい場合は反応液がゲル化し易
く、反応生成物中の水酸基含有率が低下するため塩化ビ
ニル系樹脂に配合した場合の熱安定性向上効果が期待で
きないことが判明した。従って、最適なモル比を得るた
め3〜7が望ましい。
In the present invention, it is desirable to increase the molar ratio of pentaerythritol to dibasic acid as much as possible in order to increase the content of hydroxyl groups in the molecule. In order to obtain a predetermined dehydration amount, it is necessary to perform a dehydration reaction for a long time, and as a result, the coloration becomes conspicuous with the progress of the reaction, and at a stage where the predetermined dehydration amount is obtained, the degree of coloring cannot be practically endured. Become.
Further, it has been found that when the molar ratio is less than 3, the reaction liquid tends to gel and the hydroxyl group content in the reaction product decreases, so that the effect of improving thermal stability cannot be expected when blended with a vinyl chloride resin. . Therefore, 3 to 7 is desirable to obtain the optimum molar ratio.

【0014】上記の脱水縮合反応はエステル化反応及び
エーテル化反応からなり、反応により得られる化合物
は、ペンタエリスリトール同士が分子間でエーテル結合
したジペンタエリスリトールやさらに縮合した、トリペ
ンタエリスリトールやテトラペンタエリスリトール等の
直鎖や分枝したポリペンタエリスリトールの水酸基に反
応に用いた酸がエステル結合した化合物である。また得
られた化合物は白色の結晶である。
The above dehydration condensation reaction consists of an esterification reaction and an etherification reaction, and the compound obtained by the reaction is dipentaerythritol in which pentaerythritol is ether-bonded between molecules or further condensed, tripentaerythritol or tetrapentaerythritol. It is a compound in which the acid used in the reaction is ester-bonded to the hydroxyl group of linear or branched polypentaerythritol such as erythritol. Moreover, the obtained compound is a white crystal.

【0015】また、反応に於て該多価アルコール系安定
化助剤の融点調整や未反応ペンタエリスリトールの含有
率低下のため、反応終了間際に少量の他のカルボン酸で
さらにエステル化あるいは、反応終了後30wt%以下
のジペンタエリスリトールを加え混融してもなんら構わ
ない。その場合のカルボン酸の種類は問わず、モノカル
ボン酸、ジカルボン酸、3塩基酸以上のカルボン酸、及
びそれらの混合物を用いることができる。ただし、その
添加量は、水酸基含有量を確保するため、その時点での
未反応ペンタエリスリトールとn塩基酸のカルボン酸と
のモル比がn対1で反応する量に抑えるべきである。
Further, in the reaction, the melting point of the polyhydric alcohol-based stabilizing aid is adjusted and the content of unreacted pentaerythritol is lowered, so that esterification or reaction with a small amount of other carboxylic acid may occur immediately before the reaction is completed. After the completion, 30 wt% or less of dipentaerythritol may be added and mixed together. In that case, regardless of the kind of the carboxylic acid, a monocarboxylic acid, a dicarboxylic acid, a carboxylic acid having 3 or more basic acids, and a mixture thereof can be used. However, in order to secure the hydroxyl group content, the addition amount should be suppressed to an amount at which the unreacted pentaerythritol and the carboxylic acid of the n-basic acid react at a molar ratio of n: 1.

【0016】多価アルコール系安定化助剤を配合した塩
化ビニル系樹脂組成物の透明性は、安定化助剤の融点と
配合成形時の加工温度とに関係がある。即ち、該多価ア
ルコール系安定化助剤の融点は140〜180℃である
ことが望ましく、140℃未満では融点が低すぎ粉砕時
等の製造上の問題が挙げられ、180℃より高い場合、
加工時の分散性が悪く、得られる樹脂組成物の透明性も
悪い。従って、該多価アルコール系安定化助剤は、その
融点が140〜180℃の範囲になるように、任意に原
料2塩基酸の種類を選ぶ事ができ、又、その為にペンタ
エリスリトールと2塩基酸のモル比も3:1〜7:1の
範囲で任意に選び融点を調整することができる。
The transparency of the vinyl chloride resin composition containing the polyhydric alcohol stabilizing aid is related to the melting point of the stabilizing aid and the processing temperature during compounding. That is, the melting point of the polyhydric alcohol-based stabilizing aid is preferably 140 to 180 ° C., and if the melting point is lower than 140 ° C., the melting point is too low, and there is a problem in production such as pulverization.
The dispersibility during processing is poor, and the transparency of the resulting resin composition is also poor. Therefore, the polyhydric alcohol-based stabilizing aid can arbitrarily select the kind of the basic dibasic acid so that the melting point thereof is in the range of 140 to 180 ° C., and for that purpose, pentaerythritol and The melting point can be adjusted by arbitrarily selecting the molar ratio of the basic acid within the range of 3: 1 to 7: 1.

【0017】本発明に使用する塩化ビニル系樹脂は、塩
化ビニルまたは塩化ビニリデンの単独重合物の他、エチ
レン、酢酸ビニル、アクリル等とのコポリマーやこれら
のポリマーのブレンド品であっても良く、その重合度や
粒径の大小は問わない。本発明に使用する亜鉛系安定剤
は、脂肪酸が例えば、ステアリン酸、リシノレイン酸、
パルチミン酸、オクチル酸、安息香酸、サリチル酸等で
ある金属石鹸のうち、金属部分がナトリウムと亜鉛、カ
ルシウムと亜鉛、マグネシウムと亜鉛、バリウムと亜鉛
等の様に組み合わせて使用するか、市販の亜鉛系複合安
定剤である。安定剤の形態は、液状、粉末状等の形態を
問わない。
The vinyl chloride resin used in the present invention may be a homopolymer of vinyl chloride or vinylidene chloride, a copolymer with ethylene, vinyl acetate, acryl or the like, or a blend of these polymers. The degree of polymerization or the size of the particles does not matter. The zinc-based stabilizer used in the present invention includes fatty acids such as stearic acid, ricinoleic acid,
Of metal soaps such as palmitic acid, octylic acid, benzoic acid, salicylic acid, etc., the metal part is used in combination such as sodium and zinc, calcium and zinc, magnesium and zinc, barium and zinc, or a commercially available zinc-based product. It is a complex stabilizer. The form of the stabilizer may be liquid, powder or the like.

【0018】本発明の塩化ビニル系樹脂組成物は、該組
成物の使用目的により、可塑剤を配合した軟質系にして
も良い。その場合の配合量は、塩化ビニル系樹脂100
重量部に対し、可塑剤を0〜150重量部である。ま
た、可塑剤としては、ジオクチルフタレート、ジイソデ
シルフタレート等のフタル酸エステル、アジピン酸ジオ
クチル、アゼライン酸ジオクチル等の脂肪族2塩基酸エ
ステル、りん酸トリクレジル、りん酸トリオクチル等の
りん酸エステル、エポキシ化大豆油、塩化パラフィン、
その他の可塑剤であり、これらを単独または2種以上を
併用しても良い。更には、必要に応じ他の添加剤を必要
量配合しても良い。例えば、炭酸カルシウム、水酸化ア
ルミウム等の充填剤、酸化アンチモン等の難燃剤、そし
て着色剤、抗酸化剤、亜鉛系以外の安定剤等である。
The vinyl chloride resin composition of the present invention may be a soft system containing a plasticizer depending on the purpose of use of the composition. In that case, the compounding amount is 100% vinyl chloride resin.
The plasticizer is 0 to 150 parts by weight with respect to parts by weight. Examples of the plasticizer include phthalic acid esters such as dioctyl phthalate and diisodecyl phthalate, aliphatic dibasic acid esters such as dioctyl adipate and dioctyl azelate, tricresyl phosphate, trioctyl phosphate and the like, and epoxidized macromolecules. Soybean oil, paraffin chloride,
Other plasticizers may be used alone or in combination of two or more. Furthermore, if necessary, other additives may be blended in required amounts. Examples thereof include fillers such as calcium carbonate and aluminum hydroxide, flame retardants such as antimony oxide, colorants, antioxidants and stabilizers other than zinc-based stabilizers.

【0019】[0019]

【実施例】温度計、撹拌機、留出液トラップ装置付き1
000ml四ツ口セパラブルフラスコにアジピン酸14
6g(1モル)とペンタエリスリトール816g(6モ
ル)とパラトルエンスルホン酸1.4gを仕込んで加熱
し、撹拌下160〜225℃でエステル化反応とエーテ
ル化反応を行った。反応の進行と共に副生水が留出し、
留出液量が90g(5モル)となったところで反応を停
止した。この間約3時間であった。次いで反応液をバッ
トに流し込み、室温まで冷却後粉砕して白色の粉末を得
た。これを実施例1とした。
[Example] With thermometer, stirrer, distillate trap device 1
Add adipic acid 14 to a 000 ml four-neck separable flask.
6 g (1 mol), 816 g (6 mol) of pentaerythritol and 1.4 g of paratoluenesulfonic acid were charged and heated, and an esterification reaction and an etherification reaction were carried out at 160 to 225 ° C. with stirring. By-product water is distilled off as the reaction progresses,
The reaction was stopped when the amount of distillate reached 90 g (5 mol). During this time, it was about 3 hours. Then, the reaction solution was poured into a vat, cooled to room temperature and then pulverized to obtain a white powder. This is Example 1.

【0020】以下、同様に、2塩基酸とペンタエリスリ
トールを種々のモル比にて、エステル化反応とエーテル
化反応を行い、種々の留出液量にて反応を停止し、必要
に応じて上記と同様に粉砕し各種安定化助剤を得た。
(実施例2〜6、比較例1〜6)
Similarly, the dibasic acid and pentaerythritol are subjected to the esterification reaction and the etherification reaction at various molar ratios, and the reaction is stopped at various distillate amounts. It was crushed in the same manner as above to obtain various stabilizing aids.
(Examples 2 to 6, Comparative Examples 1 to 6)

【0021】得られた各種安定化助剤をシリル化剤にて
シリル化後ガスクロマトグラフィー分析を行い、ペンタ
エリスリトール、ジペンタエリスリトール、トリペンタ
エリスリトールの含有率を調べた。又、各種安定化助剤
2gを昇華管に採取し、180〜200℃オイルバスに
3時間浸漬し昇華率を測定した。反応の条件、結果、及
び上記の結果を表−1に示した。
The various stabilizing aids thus obtained were silylated with a silylating agent and then subjected to gas chromatography analysis to examine the contents of pentaerythritol, dipentaerythritol and tripentaerythritol. Further, 2 g of each stabilizing aid was sampled in a sublimation tube and immersed in an oil bath at 180 to 200 ° C. for 3 hours to measure the sublimation rate. The reaction conditions, results, and the above results are shown in Table 1.

【0022】[0022]

【表1】 [Table 1]

【0023】次に、塩化ビニル樹脂(Geon103E
P)100g、ジオクチルフタレート50g、ステアリ
ン酸カルシウム1g、ステアリン酸亜鉛1g、及び各種
安定化助剤1g、の配合物を160℃混練ロール(東洋
精機(株)製6インチ)にて5分間混練して厚さ約0.
5mmのシートを得た。この得られたシートを、180
℃ギヤーオーブン中に入れ、加熱時間とシートの着色度
合いを観察し、熱安定性の良否を判断した。また、上記
で得られたシートを160℃プレス機にて、厚さ3mm
に成型し透明性等の外観を目視で観察した。各種安定化
助剤としては、実施例物質及び比較例物質に加え、ペン
タエリスリトール、ジペンタエリスリトール、トリペン
タエリスリトール、プレンライザーST−210(味の
素(株)製)を用い評価した。結果を表−2に示す。
Next, vinyl chloride resin (Geon 103E)
P) 100 g, dioctyl phthalate 50 g, calcium stearate 1 g, zinc stearate 1 g, and various stabilizing aids 1 g were mixed for 5 minutes with a 160 ° C. kneading roll (6 inches manufactured by Toyo Seiki Co., Ltd.). Thickness about 0.
A 5 mm sheet was obtained. This obtained sheet is
It was placed in a gear oven at ℃ and the heating time and the degree of coloration of the sheet were observed to judge the thermal stability. Also, the sheet obtained above is pressed by a press machine at 160 ° C. to a thickness of 3 mm.
After molding, the appearance such as transparency was visually observed. As various stabilizing aids, in addition to the substances of Examples and Comparative Examples, pentaerythritol, dipentaerythritol, tripentaerythritol, and Prelenizer ST-210 (manufactured by Ajinomoto Co., Inc.) were used for evaluation. Table 2 shows the results.

【0024】[0024]

【表2】 [Table 2]

【0025】[0025]

【発明の効果】以上示した様に、本発明のペンタエリス
リトールと2塩基酸(モル比3:1〜7:1)と適当な
触媒の存在下エステル化及びエーテル化反応により所定
量の水を副生除去した反応物は、熱安定性効果に優れ、
融点が加工温度に近く分散性が良好で加工時の昇華性も
ほとんどないため、塩化ビニル系樹脂組成物に配合した
場合、肌荒れ等の外観を損なうことなく安定性良好な塩
化ビニル系樹脂組成物を得ることができ、あらゆる用途
に使用できる。
As described above, a predetermined amount of water is obtained by the esterification and etherification reaction in the presence of the pentaerythritol of the present invention, a dibasic acid (molar ratio 3: 1 to 7: 1) and a suitable catalyst. The reaction product removed by-product has excellent thermal stability effect,
Since the melting point is close to the processing temperature, the dispersibility is good and there is almost no sublimation property during processing, when blended with the vinyl chloride resin composition, the vinyl chloride resin composition has good stability without impairing the appearance such as rough skin. Can be obtained and can be used for all purposes.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C08L 27/06 KGY // C07B 61/00 300 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C08L 27/06 KGY // C07B 61/00 300

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】2塩基酸またはその無水物1モルに対し、
3モル以上7モル以下のペンタエリスリトールを酸触媒
の存在下、脱水縮合を行い、2塩基酸の場合はn−1モ
ル当量以上n+1モル当量以下の水を脱水させ、2塩基
酸の無水物の場合はn−2モル当量以上nモル当量以下
の水を脱水させて得られることを特徴とする多価アルコ
ール系化合物。
1. A dibasic acid or 1 mol of its anhydride,
Dehydration condensation of 3 mol or more and 7 mol or less of pentaerythritol is carried out in the presence of an acid catalyst, and in the case of a dibasic acid, water of n-1 mol equivalent or more and n + 1 mol equivalent or less is dehydrated to dihydrate the dibasic acid anhydride. In this case, a polyhydric alcohol-based compound is obtained by dehydrating n-2 molar equivalents or more and n molar equivalents or less of water.
【請求項2】ペンタエリスリトールの含量が10重量%
以下であることを特徴とする請求項1記載の多価アルコ
ール系化合物。
2. The content of pentaerythritol is 10% by weight.
It is the following, The polyhydric alcohol type compound of Claim 1 characterized by the following.
【請求項3】塩化ビニル系樹脂100重量部に対し、カ
ルシウム−亜鉛系または/及びバリウム−亜鉛系安定剤
等の亜鉛系安定剤を0.1〜10重量部、請求項1ない
し2記載の多価アルコール系化合物を0.1〜10重量
部を配合することを特徴とする塩化ビニル系樹脂組成
物。
3. A zinc-based stabilizer such as a calcium-zinc-based or / and barium-zinc-based stabilizer is used in an amount of 0.1 to 10 parts by weight per 100 parts by weight of the vinyl chloride-based resin. A vinyl chloride resin composition comprising 0.1 to 10 parts by weight of a polyhydric alcohol compound.
JP29076794A 1994-11-25 1994-11-25 Stabilizing aid composition for vinyl chloride resin Expired - Lifetime JP3440584B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29076794A JP3440584B2 (en) 1994-11-25 1994-11-25 Stabilizing aid composition for vinyl chloride resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29076794A JP3440584B2 (en) 1994-11-25 1994-11-25 Stabilizing aid composition for vinyl chloride resin

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JPH08143704A true JPH08143704A (en) 1996-06-04
JP3440584B2 JP3440584B2 (en) 2003-08-25

Family

ID=17760274

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Country Status (1)

Country Link
JP (1) JP3440584B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009069491A1 (en) 2007-11-28 2009-06-04 Adeka Corporation Stabilizer for chlorine-containing resins and chlorine -containing resin compositions

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009069491A1 (en) 2007-11-28 2009-06-04 Adeka Corporation Stabilizer for chlorine-containing resins and chlorine -containing resin compositions
US8372907B2 (en) 2007-11-28 2013-02-12 Adeka Corporation Stabilizer for chlorine-containing resins and chlorine-containing resin composition

Also Published As

Publication number Publication date
JP3440584B2 (en) 2003-08-25

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